Chemical pulp bleaching

Abstract: Wood pulp, such as kraft, chemical or hybrid pulp, is subjected to a bleaching process wherein it is treated first with one or more oxidising agents such as oxygen, ozone or hydrogen peroxide, and then with a reducing agent such as sodium borohydride or sodium hydrosulfite. A further treatment with an oxidising agent can be carried out after the reducing treatment. Brightness may be further enhanced by treatment with an enzyme such as xylanase or with a chelant such as diethylenetriamine pentaacetic acid (DTPA).

Description: This invention relates to a process for bleaching kraft or sulfite wood pulp to enhance its brightness, to improve brightness stability and generally to improve the physical properties of the pulp. Wood pulp can be produced by numerous different processes which can be classified under the broad headings of mechanical, chemical and hybrid processes. Among the chemical processes are the kraft process wherein the wood chips or the like are treated at elevated temperature and alkaline pH with sodium sulfide, sodium hydroxide and sodium carbonate, and the sulfite process wherein the wood chips are treated at acid pH, again at elevated temperature, with sodium and magnesium bisulfites. The process of the present invention has been found to be particularly advantageous in relation to pulps produced by these chemical processes, but is not limited to any particular type of wood pulp. Hitherto, different chemical bleaching processes have been used for different types of wood pulp, and in the past these have generally comprised treatments with various combinations of chlorine, chlorine dioxide, sodium hydroxide and sodium hypochlorite. For example kraft pulp has conventionally been treated with chlorine followed by two successive cycles of sodium hydroxide and chlorine dioxide. Sulfite pulp on the other hand has been treated successively with chlorine, sodium hydroxide, sodium hypochlorite and chlorine dioxide. Because of the pollution risks associated with the use of chlorine, and in particular the risk to the ozone layer, in recent years ways have been studied to replace chlorine in such bleaching treatments and ultimately to replace chlorine compounds as well. To this end, various combinations of oxidising agents have been tried and in particular oxygen itself, ozone and hydrogen peroxide have been used in various combinations. Kassepi et al (TAPPI) Pulping Conf, (Toronto) Proc, 327-340 (Oct 1992) disclose the effect of ozonisation on kraft-oxygen (K-O) and kraft oxygen-peroxide (K-OP) pulps. The K-OP pulps generally responded better to ozone bleaching than K-O pulps. It was found that too high an ozone concentration gave rise to carbohydrate degradation and decreased viscosity of the pulp. According to Patt et al Holzforschung 45 (Suppl) 87-92 (September 1991), ozone can be used effectively in both pre-bleaching and final bleaching but both lignins and carbohydrates tend to be attacked. Carbohydrate degradation has to be suppressed by preacidification of the pulp, low-temperature bleaching, slow addition of ozone to the pulp and proper mixing. Under these conditions, an ozone concentration of 0.1% can reduce the pulp kappa number by one unit. Numerous similar studies have been carried out in recent years. WO-A-92/07139 describes a method for preserving the mechanical strength properties of chemical paper pulp comprising two steps using a peroxygenated reagent, the first of which is carried out in an acidic medium while the second is carried out in an alkaline one treatment with a reducing compound being inserted therebetween. The present invention consists in a process for bleaching kraft or sulfite wood pulp which comprises treating the pulp first with at least one oxidising agent and then with a reducing agent, characterised in that the oxidising agent comprises alkaline hydrogen peroxide or ozone and the reducing agent comprises sodium borohydride. There can thus be provided a pulp bleaching process, preferably totally chlorine free, which gives a pulp of high and stable brightness without adversely affecting the physical properties of the pulp and in particular without degrading the polysaccharides or reducing the viscosity of the pulp. A further oxidising treatment may optionally be carried out after the treatment with the reducing agent. This is preferably done with hydrogen peroxide and sodium hydroxide. The various bleaching stages are preferably all carried out at alkaline pH, for which purpose an alkaline metal hydroxide such as sodium hydroxide may be added. Brightness may be further enhanced by the use of enzymes such as xylanase and chelants such as ethylene diamine tetraacetic acid (EDTA) or, more preferably, diethylene triamine pentaacetic acid (DTPA). The sodium borohydride is preferably used in alkaline solution, and a particularly advantageous form is an aqueous solution of 10 to 25 wt.% of sodium borohydride and 15 to 45 wt.% of sodium hydroxide. One commercially available solution of this type comprises 12% of sodium borohydride and 40% of sodium hydroxide, and is supplied by Morton International, Inc under the trade mark Borol. Another such solution developed more recently comprises 20% of sodium hydroxide and 20% of sodium borohydride. Further objects and advantages of the invention will become apparent from the following detailed description and examples. The accompanying drawings illustrate results obtained in some of the examples. In the drawings: FIGS. 1 and 2 illustrate the brightness gains obtained with varying borohydride addition rates in Example 1; FIG. 3 illustrates the relationship between tensile strength and beating degree for treated and untreated kraft pulps in Example 2; FIG. 4 illustrates the relationship between tear index and beating degree for the pulps of Example 2; FIGS. 5 and 6 illustrate the brightness gains obtained in Example 3; For simplicity, the various different treatment steps which can be used in accordance with the invention are given the following letter codes: D C10 2 Not used in the most preferred embodiments which are totally chlorine-free. EOP Alkaline extraction, enhanced with peroxide and oxygen. ER Alkaline extraction, enhanced with sodium borohydride. O Oxygen, O 2 Preferred concentration 2-5% based on oven-dried pulp (ODP). Typically about 3% may be used with NaOH, at a preferred concentration of 2.0-3.0%. P Hydrogen Peroxide H 2 O 2 Preferred concentration 2.0-3.0% on ODP. Generally used with NaOH at a preferred concentration of 2.0-3.0%. Preferred temperature about 70°C. OP O 2 /NaOH/H 2 O 2 OPN O 2 /NaOH/H 2 O 2 /Nitrilamine Q Chelant EDTA or, more preferably DTPA, at preferred concentration of 0.2 to 0.6% on ODP. R Sodium Borohydride Preferably in the form of the Borol solution described above, concentration 0.5-2.0% on ODP. X Enzyme treatment Preferably with xylanase, optionally together with a chelant. Y Sodium hydrosulfite Preferably generated in situ by reaction of sodium bisulfite with an aqueous borohydride/sodium hydroxide solution. Z Ozone, O 3 Preferred addition rate 0.2-1.0% on ODP, depending on the kappa number of the incoming pulp. Treatment temperature preferably less than 50°C. The following bleaching sequences in accordance with the invention have been found particularly advantageous: OZRD; OZRP; OXPRP; OXPR; OQPR; OQPRP; (OP) (OP N ) ZRP The following processes are preferred for bleaching particular types of pulp: SULFITE PULP (SOFTWOOD OR HARDWOOD) ECF Processes (free of elemental chlorine): OZRD OZRDY OZDR TCF Processes (totally chlorine-free) OZPR ZPR OZRP QPR ZRP (EOP) PR OZRPY KRAFT PULP (SOFTWOOD OR HARDWOOD) ECF Processes: D(EOP)D(ER)D OZR(EOP)D D(EOP)D(ER)DY TCF Processes: O(OP)ZRP OZRP O(OP)ZRPY OZPR OQPR OXPR OZRPY In the following examples concentrations are based on ODP (oven-dried pulp) unless otherwise stated. EXAMPLE 1 Totally chlorine free (TCF) bleaching process sequences OXPR and OXPRP were carried out on kraft pulp of NCC pine. The oxidative bleaching sequence was as follows: O: O 2 at 3%, NaOH at 2.0-2.5%; X: Xylanase; P: H 2 O 2 at 2.0 to 3.0%, NaOH at 2.0 to 3.0%, DTPA at 0.4%. The pulp was taken out after SO 2 addition after the last peroxide stage and had a pH value of 4.5 and a consistency of 31.8%. The initial ISO brightness was 73.9% but was not stable and varied between 70.9 and 71.8% several days later. The pulp was diluted down to 10% consistency with distilled water and a series of reductive bleaching trials was carried out at 70°C, for a retention time of 60 minutes in each case. The trials were conducted using sodium borohydride, alone and in combination with sodium bisulfite and with hydrogen peroxide. A 2% wt. aqueous borohydride solution (NaBH 4 :NaOH ratio 3:10, pH = 12.8) and 4% wt. NaHSO 3 solution (pH = 4.2) were prepared for the treatment. Aging tests were conducted according to TAPPI standard method (4 hrs at 105°C). Aqueous solutions of 11.5% H 2 O 2 and 10% NaOH were used for the peroxide bleaching. A 32% DTPA solution considered as 100% was diluted with distilled water to a 1% solution to be used for the peroxide stage. After the pH adjustment to 4.5 with 1% H 2 SO 4 , handsheets were prepared. The trials were performed with 20g samples in sealed polyethylene bags plunged into an agitating water bath. The first series of the trials was conducted with different amounts of alkaline borohydride solution (NaBH 4 12%, NaOH 40%, water 48%). The bleaching conditions and the results are listed in Table 1 below and the brightness response versus the NaBH 4 solution addition rate is illustrated in Figure 1, which also illustrates the brightness after aging. Figure 1 shows that the brightness response is increased very fast by adding the borohydride solution to 0.6%. A further increasing of chemical charge to 1% can achieve 0.5% brightness extra. A maximum brightness gain of 2.6% ISO points can be achieved by adding 1% of the borohydride solution. RUN N° NaBH 4 /NaOH Solution pH BRIGHTNESS Δ-BRIGHTNESS %/o.d.pulp Initial Final Before aging % ISO After aging % ISO Before aging % ISO After aging % ISO blank - 4.5 4.5 73.9 72.8 0.0 0.0 1 0.2 9.1 5.6 74.3 73.0 0.4 0.2 2 0.4 10.2 9.3 74.9 74.0 1.0 1.2 3 0.6 11.0 11.0 76.0 74.8 2.1 2.0 4 0.8 11.5 11.4 76.4 75.1 2.5 2.3 5 1.0 11.8 11.5 76.5 75.3 2.6 2.5 The brightness reversion of the untreated kraft pulp was 1.1 points. The reductive treatment with sodium borohydride solution can offer a relatively stable brightness gain, if one compares the brightness gain before and after aging. The second series of the trials was performed with 1% of the borohydride solution and subsequently with 1% hydrogen peroxide with and without washing between these two stages. As reference, the pulp was also bleached with 1% hydrogen peroxide alone. The bleaching conditions and the results are compiled in Table 2. The combined treatment was carried out for 180 min. and the peroxide-only treatment for 240 min. A treatment with 1% hydrogen peroxide can increase the final brightness by 3.6 points. A reductive treatment with 1% of the borohydride solution increases the brightness by 3 points. A subsequent peroxide bleaching can increase the brightness by 2.8 points more. The brightness response is slightly reduced (0.2 points) if the pulp is not washed between the borohydride solution stage and the peroxide stage. For the mill practice, this combination is very interesting, because the mill can not only save the investment cost for the washer, but also use residual NaOH of the borohydride solution. RUN N° STAGE CHEMICALS (% / o.d. pulp) pH BRIGHTNESS (% ISO) Δ-BRIGHTNESS (% ISO) NaBH 4 /NaOH solut. H 2 O 2 NaOH DTPA Initial Final Before aging After aging Before aging After aging blank - - - - 4.5 4.5 71.8 71.5 - - 6 P - 1.0 1.0 0.3 12.5 12.4 75.4 74.9 3.6 3.4 blank - - - - 4.5 4.5 70.9 70.7 - - 7 R 1.0 - - - 11.7 73.9 73.3 3.0 2.6 / P - 1.0 0.45 0.3 11.4 10.8 76.5 75.5 5.6 4.8 without washing 8 R 1.0 - - - 11.9 11.1 / P - 1.0 0.85 0.3 11.9 11.0 76.7 75.7 5.8 5.0 with washing Constant bleaching conditions: R-Stage P-Stage Temperature, °C 70 70 Consistency, % 10 10 Time, min. 60 180 (n°6) 240 (n° 7-8) Consumption of H 2 O 2 , % - 49.8 (n°6) 64.2 (n°7) 61.6 (n°8) The third series of the bleach trials was carried out with sodium bisulfite as a reference and a combination of sodium bisulfite and the sodium borohydride solution. The addition rate of NaHSO 3 was kept constant by 1.5%/o.d. pulp, while the NaBH 4 addition rate was varied between 0.1% and 0.5%. The treatment rates and brightness gains are given in Table 3. RUN N° CHEMICAL (% / o.d. pulp) pH BRIGHTNESS (% ISO) Δ-BRIGHTNESS (% ISO) NaBH 4 /NaOH solution NaHSO 3 Initial Final Before aging After aging Before aging After aging blank - - 4.5 4.5 73.9 72.8 - - 9 (ref.) - 1.5 4.2 3.7 74.2 72.7 0.3 -0.1 10 0.1 1.5 4.5 3.7 74.0 72.9 0.1 0.1 11 0.2 1.5 5.2 4.2 74.9 73.6 1.0 0.8 12 0.3 1.5 5.6 4.5 75.0 73.8 1.1 1.0 13 0.4 1.5 6.0 4.7 75.3 74.2 1.4 1.4 14 0.5 1.5 6.5 5.4 75.8 74.6 1.9 1.8 Constant bleaching conditions Temperature 70°C Time 60 min. Consistency 10 % Sodium bisulfite is a weak reductant. A reductive treatment of the TCF bleached kraft pulp with 1.5% NaHSO 3 can increase the final brightness by 0.3 points. A combination of sodium bisulfite and alkaline borohydride solution can improve the bleaching efficiency to gain 1.9 brightness points. In comparison with adding 0.6% borohydride solution only, little synergistic bleaching effect is obtained by adding two reductants serially. This has already been established in the case of mechanical pulp and deinked pulp. The reason might be due to the lower residual lignin content of the bleached chemical pulp. The brightness gains before and after aging are illustrated in Figure 2 which shows that the brightness stability of the treated only with 1.5 NaHSO 3 pulp is inferior to that of the combination of NaHSO 3 and borohydride solution. EXAMPLE 2 (reference) To investigate the physical properties of the reductive treated pulp, 100g oven dry pulp as used in Example 1 were treated with 1% of an alkaline NaBH 4 solution having the composition of the Borol solution described above. The reaction time was prolonged to 90 min. to compensate for the difficult mixing of the pulp at the medium consistency of 10% in the laboratory. The treatment temperature was 70°C as in Example 1, with an initial pH of 11.8 and a final pH of 11.6 The yield of the borohydride treated pulp was 99.7% and the final brightness before and after aging was 74.6% and 73.3% ISO respectively. The physical properties of the untreated and treated pulps are set out in Tables 4 and 5 respectively. In comparison with the untreated TCF bleached pulp, the beating energy as well as the strength properties, especially tensile strength and burst index of the borohydride treated pulp, were positively influenced, whereas the tear index of the treated and untreated pulps remained at the same level, as can be seen from Figures 3 and 4. The optical properties, i.e. opacity, absorption coefficient and light-scattering coefficient of the borohydride-treated pulp were reduced slightly due to the higher final brightness of the treated pulp (2.8 points higher). The viscosity of the borohydride treated pulp was increased from 748 dm 3 /kg to 762 dm 3 /kg. This can explain the improvement of the strength properties after the borohydride treatment. Kappa number and all strength properties were determined according to ZELLCHEMING standards. Brightness, viscosity and light-scattering, were tested according to SCAN-C 11:75, SCAN-CM : 88 AND SCAN-C 27:76, respectively. BEATING DEGREE 1 2 3 4 5 1 interpolat. 2 interpolat. 3 interpolat. BEATING DEGREE [°SR] 15.8 17.0 20.3 30.3 53.0 20.0 25.0 30.0 BEATING TIME [min] 0 15 30 45 60 29 37 45 SPEC. VOLUME (bulk) [cm 3 /g] 1.49 1.25 1.21 1.17 1.12 1.21 1.19 1.17 BREAKING LENGTH [km] 4.13 7.90 8.79 9.29 9.65 8.72 9.03 9.28 BURSTING PRESSURE [kPa] 263 446 466 459 469 465 463 459 BURSTING PRESSURE 75 g [kPa] 235 420 444 440 456 442 442 440 BURSTING PRESSURE 80 G [kPa] 251 448 474 470 486 472 472 440 TEARING RESISTANCE [cN] 214.5 127.5 122.1 108.8 99.6 122.6 115.8 109.1 STRENGTH FACTOR 9.42 10.03 10.36 10.05 9.81 10.33 10.21 10.06 TENSILE-INDEX [Nm/g] 40.5 77.4 86.1 91.1 94.6 85.5 88.5 91.0 TEAR-INDEX [mN.m 2 /g] 25.6 16.0 15.5 13.8 12.9 15.6 14.7 13.9 BURST-INDEX [kPa.m 2 /g] 3.1 5.4 5.8 5.7 6.0 5.8 5.8 5.7 ABSORPTION COEFFICIENT [m 3 /kg] 0.47 0.47 0.53 0.51 0.60 0.53 0.52 0.51 OPACITY, 80 g/m 2 [%] 82.0 72.1 71.4 70.1 69.0 71.4 70.8 70.1 LIGHT-SCATTERING COEFF. [m 2 /kg] 28.9 18.4 17.5 16.5 15.4 17.5 17.0 16.5 BRIGHTNESS [% ISO] 71.8 CUEN VISCOSITY [dm 3 /kg] 748 KAPPA N° 5.4 BEATING DEGREE 1 2 3 4 5 1 interpolat. 2 interpolat. 3 interpolat. BEATING DEGREE [°SR] 16.0 18.0 23.5 32.5 52.0 20.0 25.0 30.0 BEATING TIME [min] 0 15 30 45 60 20 33 41 SPEC. VOLUME (bulk) [cm 3 /g] 1.48 1.20 1.15 1.15 1.10 1.18 1.15 1.15 BREAKING LENGTH [km] 4.31 8.16 8.50 9.48 10.24 8.28 8.67 9.21 BURSTING PRESSURE [kPa] 289 428 491 465 549 450 486 472 BURSTING PRESSURE 75 g [kPa] 256 404 467 448 532 427 463 453 BURSTING PRESSURE 80 G [kPa] 273 431 498 477 568 455 494 483 TEARING RESISTANCE [cN] 223.6 121.2 108.6 107.0 98.0 116.6 108.4 107.4 STRENGTH FACTOR 9.82 9.94 9.61 10.07 10.02 9.80 9.69 9.95 TENSILE-INDEX [Nm/g] 42.3 80.1 83.4 93.0 100.4 81.2 85.0 90.3 TEAR-INDEX [mN.m 2 /g] 26.4 15.3 13.8 13.6 12.6 14.7 13.7 13.6 BURST-INDEX [kPa.m 2 /g] 3.3 5.2 6.1 5.9 6.9 5.5 6.1 6.0 ABSORPTION COEFFICIENT [m 3 /kg] 0.44 0.38 0.38 0.40 0.44 0.38 0.38 0.39 OPACITY, 80 g/m 2 [%] 82.2 69.8 68.1 66.3 65.2 69.2 67.8 66.8 LIGHT-SCATTERING COEFF. [m 2 /kg] 29.2 17.5 16.2 15.3 14.3 17.0 16.1 15.6 BRIGHTNESS [% ISO] 74.6 CUEN VISCOSITY [dm 3 /kg] 762 KAPPA N° EXAMPLE 3 Bleaching trials similar to those of Example 1 but using a sequence OQPR were carried out on 20g samples of spruce kraft pulp. The O and P stages were as in Example 1 and the Q stage was carried out with EDTA. The pulp was taken out after SO 2 addition, at a pH value of 5.5. The treatment conditions were the same as those of Example 1. The pH value of the pulp was adjusted to 5.5 with 0.1% H 2 SO 4 before handsheets were prepared for brightness determination. The initial ISO brightness of the untreated pulp was 75.6% before aging and 74.2% after aging for 4 hours at 105°C. The first series of the trials was performed by adding the alkaline borohydride solution only. The addition rate of this solution was varied between 0.2% to 1%. Another series of the bleach trials was carried out with a serial combination of sodium bisulfite and the borohydride solution. The addition rate of NaHSO 3 was kept constant at 1.5%/o.d. pulp, while the borohydride solution addition rate was varied between 0.2% to 0.6%. 2% alkaline borohydride solution and 4% sodium bisulfite solution were prepared daily. The results are shown in Table 6 and illustrated in Figures 5 (NaBH 4 solution only) and 6 (NaBH 4 /bisulfite). The maximum achieved brightness response was 3.6% ISO points by adding 0.6% of the NaBH 4 solution. A further increase of the amount of NaBH 4 solution reduced the bleaching efficiency of this solution, most probably because the high alkalinity of the solution causes a negative alkaline darkening effect. The use of 1.5% sodium bisulfite as a reference improved the brightness response by 1.3 brightness points. A combination of sodium bisulfite and alkaline NaBH 4 solution could increase the brightness gain by 3 points (see Fig. 6) but concerning the brightness response, there was little evidence of the synergistic bleaching effect of adding two reductants, which has been observed when bleaching mechanical and deinked pulp. RUN N° CHEMICAL pH BRIGHTNESS (% ISO) BRIGHTNESS INCREASE VERSUS BLANK (% ISO) BRIGHTNESS REVERSION (% ISO) NaBH 4 /NaOH sol. % NaHSO 3 % Initial Final Before aging After aging Before aging After aging Blank - - 5.5 5.5 75.6 74.2 0 0 1.4 1 0.2 - 10.6 8.9 77.1 75.7 1.5 1.5 1.4 2 0.4 - 11.4 11.0 78.8 76.7 3.2 2.5 2.1 3 0.6 - 11.6 10.6 79.2 77.3 3.6 3.1 1.9 4 0.8 - 11.8 11.5 79.1 77.0 3.5 2.8 2.1 5 1.0 - 11.9 11.2 78.7 76.2 3.1 2.0 2.5 6 (ref.) - 1.5 4.8 4.0 76.9 75.0 1.3 0.8 1.9 7 0.2 1.5 4.8/5.7 4.7 78.2 76.5 2.6 2.3 1.7 8 0.3 1.5 4.8/6.7 5.8 78.4 77.0 2.8 2.8 1.4 9 0.4 1.5 4.8/6.2 5.0 78.2 76.4 2.6 2.2 1.8 10 0.5 1.5 4.8/7.1 5.9 78.6 76.6 3.0 2.4 2.0 11 0.6 1.5 4.8/7.4 6.5 78.5 76.6 2.9 2.4 1.9 Constant conditions Temperature 70 °C Time 60 min. Consistency 10 % Pulp sample 20 g oven dry pulp The aging test was conducted for 4 hours at 105°C, according to the TAPPI-method. The brightness of the untreated and reductively treated pulps decreased after the aging. Fig 5 and 6 show the brightness reversion varies between 1.4 and 2.5 points. The brightness reversion of the OP bleached pulp was 1.4 points. The brightness reversion of the reductively treated pulps varied between 1.4 and 2.5% ISO. However the final brightness of reductively treated pulps (after aging) was still 2.8 - 3.1 points higher than the final brightness of untreated pulp. EXAMPLE 4 (reference) To investigate the physical properties after the reductive treatment, 100g o.d. pulp as used in Example 3 were treated with 1% of the Borol NaBH 4 solution described above. The results before treatment are listed in Table 7 and those after are listed in Table 8. The conditions were the same as in Example 2 and the pH was 11.7 before and after treatment. The physical properties were measured as in Example 2. The yield of the borohydride-treated pulp was 99.8% and the final brightness was 78.5% ISO before aging and 77.8% after. In comparison with the untreated kraft pulp, the beating energy as well as the strength properties of the borohydride-treated pulp were not influenced significantly. Due to the higher final brightness, the optical properties like opacity, absorption coefficient and light-scattering coefficient were reduced a little. The viscosity of the treated pulp was increased slightly as expected. The variations of tear index and tensile strength with beating degree were similar to those obtained in Example 2 (see Figs. 3 and 4). EXAMPLE 5 Reductive bleaching trials using sequences OQPR and OQPRP were carried out on samples of kraft hardwood (birch) pulp, the oxidative sequence being carried out as in Example 3. The pulp samples came from Sweden. The kappa number after the cooking process was 15 and 10 after the O-stage. The residual kappa number of the OQP bleached pulp was determined as 5.4 in the laboratory. The trials were conducted by using the Borol NaBH 4 solution described above, directly or in combination with hydrogen peroxide. Two pulps, namely wet pulp (ledge) and pulp sheet, with an initial brightness of 79.7% ISO and 81.6% ISO were used for the laboratory bleach trials. A first series of the trials was performed by adding the NaBH 4 solution to both pulp samples. The addition rate was varied between 0.2% and 1.2% (the solution contains 12% wt NaBH 4 , 40% wt NaOH and 48% wt H 2 O). The second series of the bleach trials was done by adding 1% peroxide or 0.5-1% NaBH 4 solution and 1% peroxide with and without washing between these two stages. The bleach trials were performed in sealed PE-bags plunged into an agitating water bath. The following conditions were applied: Temperature 70°C Consistency of pulp 10% (15% for R-stage) Time 60 min for NaBH 4 and combination stage 240 min for peroxide stage Sample weight 10 g and 100 g o.d. pulp A 2% wt NaBH 4 solution (Borol, described above, pH = 12.8) was prepared freshly each time for the treatment. Aging tests were conducted according to TAPPI standard method (4 hrs at 105°C). The results are shown in Table 9. RUN N° CHEMICAL pH BRIGHTNESS (% ISO) BRIGHTNESS INCREASE VS. BLANK (% ISO) BRIGHTNESS REVERSION (% ISO) NaBH 4 sol. (%/pulp) Initial Final Before aging After aging Before aging After aging WET PULP (ledge) Blank - 6.4 6.0 79.7 78.6 0 0 1.1 1 0.2 10.8 9.7 81.4 79.4 1.7 0.8 2.0 2 0.4 11.3 10.0 82.9 81.0 3.2 2.4 1.9 3 0.6 11.6 10.4 82.4 80.8 2.7 2.2 1.6 4 0.8 11.9 10.6 82.9 80.9 3.2 2.3 2.0 5 1.0 12.0 10.8 83.0 81.0 3.3 2.4 2.0 6 1.2 12.1 11.8 82.2 80.8 2.5 2.2 1.4 PULP SHEET Blank - 6.9 6.5 81.6 79.9 0 0 1.7 7 0.2 10.6 9.4 83.0 80.2 1.4 0.3 2.8 8 0.4 10.9 10.4 83.6 81.0 2.0 1.1 2.6 9 0.6 11.1 10.8 83.9 81.5 2.3 1.6 2.4 10 0.8 11.4 10.9 84.0 81.7 2.4 1.8 2.3 11 1.0 11.5 11.2 84.1 82.0 2.5 2.1 2.1 Constant conditions Temperature 70°C Time 60 min Consistency 10% Pulp sample 10 g oven dry pulp The second series of the laboratory bleach trials was carried out with peroxide as well as with a combination of the NaBH 4 solution and peroxide. The bleaching conditions and the results are listed in Table 10. The physical properties of the treated and untreated pulp are listed in Tables 11 to 13. 1% H 2 O 2 can increase the brightness of 2.6 points. Reductive treatments with 0.5 and 1% of the NaBH 4 solution increased the brightness response of 2.1 and 2.8 points respectively. Subsequently the pulps were bleached with 1% H 2 O 2 . The final brightness was 85.1% ISO and 85.4% ISO respectively. If the pulp was not washed between the R-stage and the P-stage, the brightness response was reduced by 0.2 and 0.4 points. With respect to the viscosity, the initial pulp had a viscosity of 770 dm 3 /kg. After the NaBH 4 treatment, the viscosity of the pulp was increased to 800 dm 3 /kg. But the viscosity of the pulp dropped again to 756 dm 3 /kg after the P-stage. In comparison with peroxide bleaching the viscosity difference was not significant. The yield of the peroxide treated and with the combination of NaBH 4 solution and peroxide treated pulp ranged between 99.8-99.7%. RUN N° STAGE CHEMICALS (%/o.d. pulp) pH BRIGHTNESS (% ISO) Δ-BRIGHTNESS (% ISO) NaBH 4 sol. H 2 O 2 NaOH DTPA Initial Final Before aging After aging Before aging After aging BLANK - - - - 81.6 79.9 - - 30 P - 1 1 0.4 11.7 10.7 84.2 82.5 2.6 2.6 31 R 0.5 - - - 11.0 10.3 83.7 81.7 2.1 1.8 P without washing - 1 0.8 0.4 11.4 11.0 84.9 83.3 3.3 3.4 32 R 1.0 - - - 11.5 10.7 84.4 82.5 2.8 2.6 P without washing - 1 0.65 0.4 11.4 11.2 85.0 83.1 3.4 3.2 33 R 0.5 - - - 11.0 10.3 83.7 81.7 2.1 1.8 P with washing - 1 0.8 0.4 11.5 10.8 85.1 83.0 3.5 3.1 34 R 1 - - - 11.5 10.7 84.4 82.5 2.8 2.6 P with washing - 1 0.8 0.4 11.6 11.0 85.4 83.3 3.8 3.4 Constant bleaching conditions: R-Stage P-Stage Temperature, °C 70 70 Consistency, % 15 10 Time, min. 60 240 Consumption of H 2 O 2 45.2 (N° 30) 64.2 (N° 31) 67.0 (N° 32) 63.0 (N° 33) 77.3 (N° 34) 1. BEATING DEGREE 2. BEATING DEGREE 3. BEATING DEGREE 4. BEATING DEGREE 5. BEATING DEGREE 1. Interpolat. BEATING DEGREE 2. Interpolat. BEATING DEGREE 3. Interpolat. BEATING DEGREE BEATING DEGREE [°SR] 18.0 24.0 31.5 40.5 64.0 BEATING TIME [min] 0 15 30 45 60 SPEC. VOLUME [cm 3 /g] 1.48 1.21 1.24 1.23 1.13 BREAKING LENGTH [km] 3.64 8.32 8.83 9.17 9.71 BURSTING PRESSURE [kPa] 149 388 378 396 442 BURSTING PRESS. 75g [kPa] 142 370 370 384 439 BURSTING PRESS. 80g [kPa] 151 395 395 410 468 TEARING RESISTANCE [cN] 72.2 87.2 97.3 106.7 77.9 STRENGTH FACTOR 5.13 8.52 9.27 9.89 8.70 TENSILE INDEX [Nm/g] 35.7 81.6 86.6 89.9 95.2 TEAR INDEX [mN*m 2 /g] 9.2 11.1 12.7 13.9 10.3 BURST INDEX [kPa*m 2 /g] 1.9 4.8 4.8 5.0 5.7 ABSORPTION COEFFICIENT [m 3 /kg] 0.22 0.21 0.22 0.21 0.28 OPACITY, 80 g/m 2 [%] 81.0 71.6 71.1 69.1 63.2 LIGHT-SCAT. COEFFICIENT [m 2 /kg] 33.8 21.3 19.6 18.6 13.9 BRIGHTNESS [% ISO] ≈ 81.6 CUEN-VISCOSITY [dm 2 /kg] 770 KAPPA N° [-] 5.4 1. BEATING DEGREE 2. BEATING DEGREE 3. BEATING DEGREE 4. BEATING DEGREE 5. BEATING DEGREE 1. Interpolat. BEATING DEGREE 2. Interpolat. BEATING DEGREE 3. Interpolat. BEATING DEGREE BEATING DEGREE [°SR] 18.0 24.0 33.0 42.3 65.5 20.0 25.0 30.0 BEATING TIME [min] 0 15 30 45 60 5 17 25 SPEC. VOLUME [cm 3 /g] 1.45 1.24 1.24 1.24 1.11 1.38 1.24 1.24 BREAKING LENGTH [km] 3.80 8.63 90.6 9.55 9.59 5.41 8.67 8.92 BURSTING PRESSURE [kPa] 169 380 412 388 434 239 384 401 BURSTING PRESS. 75g [kPa] 159 359 398 378 426 226 363 385 BURSTING PRESS. 80 g [kPa] 170 382 425 403 454 241 387 411 TEARING RESISTANCE [cN] 54.3 85.6 93.5 105.5 85.5 64.7 86.4 90.9 STRENGTH FACTOR 4.54 8.59 9.21 10.04 9.06 5.89 8.66 9.00 TENSILE INDEX [Nm/g] 37.3 84.6 88.9 93.7 94.0 53.1 85.0 87.4 TEAR INDEX [mN*m 2 /g] 6.8 10.8 12.1 13.6 11.2 8.1 10.9 11.6 BURST INDEX [kPa*m 2 /g] 2.1 4.7 5.2 5.0 5.5 2.9 4.7 5.0 ABSORPTION COEFF. [m 3 /kg] 0.16 0.16 0.15 0.16 0.22 0.16 0.16 0.15 OPACITY. 80 g/m 2 [%] 79.1 70.7 68.9 67.2 64.9 76.3 70.5 69.5 LIGHT-SCAT. COEFF. [m 2 /kg] 33.3 21.4 19.6 18.3 14.5 22.2 2.2 13.1 BRIGHTNESS [% ISO] 85.1 CUEN-VISCOSITY [dm 2 /kg] 756 KAPPA N° [-] 1. BEATING DEGREE 2. BEATING DEGREE 3. BEATING DEGREE 4. BEATING DEGREE 5. BEATING DEGREE 1. Interpolat. BEATING DEGREE 2. Interpolat. BEATING DEGREE 3. Interpolat. BEATING DEGREE BEATING DEGREE [°SR] 18.0 25.8 33.5 45.0 71.8 20.0 25.0 30.0 BEATING TIME [min] 0 15 30 45 60 4 14 23 SPEC. VOLUME [cm 3 /g] 1.50 1.24 1.22 1.23 1.05 1.44 1.26 1.23 BREAKING LENGTH [km] 3.85 8.38 9.02 9.36 10.47 5.02 7.94 8.73 BURSTING PRESSURE [kPa] 163 391 382 389 448 222 369 386 BURSTING PRESS. 75g [kPa] 154 368 367 378 443 209 347 367 BURSTING PRESS. 80 g [kPa] 165 392 392 404 473 223 370 392 TEARING RESISTANCE [cN] 63.8 98.3 93.1 95.1 81.9 72.7 95.0 95.4 STRENGTH FACTOR 4.95 9.08 9.16 9.43 9.26 6.02 8.68 9.12 TENSILE INDEX [Nm/g] 37.7 82.2 88.5 91.8 102.6 49.2 77.9 85.6 TEAR INDEX [mN*m 2 /g] 8.1 12.3 11.9 12.2 10.8 9.2 11.9 12.1 BURST INDEX [kPa*m 2 /g] 2.0 4.8 4.7 5.0 5.8 2.7 4.5 4.8 ABSORPTION COEFF. [m 3 /kg] 0.17 0.16 0.17 0.17 0.37 0.17 0.16 0.17 OPACITY. 80 g/m 2 [%] 79.8 70.9 67.8 68.0 62.4 77.5 71.8 69.2 LIGHT-SCAT. COEFF. [m 2 /kg] 33.6 21.0 18.7 17.7 11.7 30.3 22.2 19.8 BRIGHTNESS [% ISO] 84.2 CUEN-VISCOSITY [dm 2 /kg] 748 KAPPA N° [-] With an increasing chemical addition rate of NaBH 4 solution to 1%/o.d. pulp, a brightness gain between 2.5 and 3.3% ISO was achieved. A further increase of the NaBH 4 solution addition rate did not improve the bleaching efficiency due to the high alkalinity of the NaBH 4 solution. After the aging test (4 hours at 105°C), a higher brightness loss on the pulp sheet than on the wet pulp was determined. The reason was that the latter pulp had already lost its brightness before the bleach performance. However we were able to increase the final brightness (after aging) of the pulp with 2.1%-2.4% ISO by using 1% of the NaBH 4 solution. In the combined treatment, total brightness increases of 3.5 and 3.8% ISO were gained by using 0.5 and 1% of alkaline NaBH 4 solution in R-stage and 1% H 2 O 2 in P-stage. The brightness response was reduced slightly to 3.3-3.4% ISO if the pulp was not washed between R- and P-stage. By applying 1% H 2 O 2 for the final bleaching stage, a brightness gain of 2.6 points was achieved, which was 0.9-1.2% ISO lower than with the combination. The physical properties of the P and RP treated pulps did not change in comparison with the untreated pulp. The optical properties, i.e. opacity, absorption coefficient and light-scattering coefficient of the P and RP treated pulps were reduced slightly due to the higher final brightness of the treated pulps. EXAMPLE 6 Bleaching sequences with and without a borohydride treatment stage were carried out to compare the brightness level and viscosity of the resulting pulp. One pulp sample was subjected to the bleaching sequence (OP) (OP N ) ZRP with the results shown in Table 14. Stage No. Treatment Step Residual kappa No. Brightness % ISO Viscosity dm 3 /kg O Unbleached 15 28 886 1 OP (O 2 ,NaOH,H 2 O 2 ) 4.5 50.7 765 2 OP N (O 2 , NaOH, H 2 O 2 , nitrilamine) 2.9 63.7 734 3 Z (O 3 at 0.2%) 1 80.7 639 4 R (1% Borol at 70°C) - 83 680 5 P (1%H 2 O 2 , 1% NaOH at 70°C) - 87.3 662 A second sample was subjected to steps 1 to 3 and 5 in Table 14, the R stage 4 being omitted. The resulting brightness was also 87.3% ISO, but the viscosity was only 568 dm 3 /kg. Thus, the process of the invention gave an equivalent brightness level to that achieved with oxidative bleaching only, but with a much lower viscosity loss. Indeed, it can be seen from Table 14 that the NaBH 4 bleaching stage itself gives a substantial gain in viscosity.

Claims: A process for bleaching kraft or sulfite wood pulp which comprises treating the pulp first with at least one oxidising agent and then with a reducing agent, characterised in that the oxidising agent comprises alkaline hydrogen peroxide or ozone and the reducing agent comprises sodium borohydride. A process as claimed in claim 1 wherein the sodium borohydride is used in an aqueous alkaline solution. A process as claimed in claim 2 wherein said aqueous solution comprises 10 to 25 wt.% of sodium borohydride and 15 to 45 wt.% of sodium hydroxide. A process as claimed in claim 3 wherein said aqueous solution comprises about 12% sodium borohydride and about 40% sodium hydroxide and is used in an amount of 0.5 to 2.0% based on oven dried pulp (ODP). A process as claimed in any preceding claim wherein a further oxidation treatment is carried out after the treatment with said reducing agent. A process as claimed in claim 5 wherein said further oxidising treatment is carried out using hydrogen peroxide. A process as claimed in any preceding claim wherein said treatments with oxidising and reducing agents are carried out at alkaline pH. A process as claimed in any preceding claim wherein said pulp is treated with an enzyme to enhance brightness. A process as claimed in claim 8 wherein said enzyme is xylanase. A process as claimed in any preceding claim wherein said pulp is treated with a chelant to enhance brightness A process as claimed in claim 10 wherein said chelant is diethylenetriamine pentaacetic acid (DTPA).

Inventors: GUILBAULT LAWRENCE J, HACHE MAURICE, MUNROE DAVID C, TEODORESCU GRAZIELLA, WANG DAVID L K, GUILBAULT, LAWRENCE J., HACHE, MAURICE, MUNROE, DAVID C., TEODORESCU, GRAZIELLA, WANG, DAVID L.K.
Applicants: MORTON INT INC, MORTON INTERNATIONAL, INC.
Application year: 1994
Main classification: D21C9
IPC codes: D21C9, D21C5